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Dynamic simulation on effect of flame arrangement on thermal process of regenerative reheating furnace

机译:火焰排列对蓄热式加热炉热过程影响的动态模拟

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摘要

By analyzing the characteristics of combustion and billet heating process, a 3-D transient computer fluid dynamic simulation system based on commercial software CFX4.3 and some self-programmed codes were developed to simulate the thermal process in a continuous heating furnace using high temperature air combustion technology. The effects of different switching modes on injection entrancement of multi burners, combustion and billet heating process in furnace were analyzed numerically, and the computational results were compared with on-site measurement, which verified the practicability of this numerical simulation system.The results indicate that the flow pattern and distribution of temperature in regenerative reheating furnace with partial same-side-switching combustion mode are favorable to satisfy the high quality requirements of reheating, in which the terminal heating temperature of billets is more than 1 460 K and the temperature difference between two nodes is not more than 10 K. But since the surface average temperature of billets apart from heating zone is only about 1 350 K and continued heating is needed in soaking zone, the design and operation of current state are still needed to be optimized to improve the temperature schedule of billet heating. The distribution of velocity and temperature in regenerative reheating furnace with same-side-switching combustion mode cannot satisfy the even and fast heating process. The terminal heating temperature of billets is lower than that of the former case by 30 K. The distribution of flow and temperature can be improved by using cross-switching combustion mode, whose terminal temperature of billets is about 1 470 K with small temperature difference within 10 K.
机译:通过分析燃烧和钢坯加热过程的特点,开发了基于商用软件CFX4.3和一些自编程代码的3D瞬态计算机流体动力学模拟系统,以模拟使用高温空气的连续加热炉中的热过程。燃烧技术。数值分析了不同切换方式对多燃烧器喷射入口,燃烧和炉膛加热过程的影响,并将计算结果与现场测量结果进行了比较,证明了该数值模拟系统的实用性。具有部分相同侧切换燃烧模式的蓄热式加热炉的流型和温度分布有利于满足加热的高质量要求,其中坯料的最终加热温度大于1 460 K,并且两个节点的最大温度不超过10K。但是,由于加热区以外的坯料的表面平均温度仅为1 350 K,并且均热区需要持续加热,因此仍需要优化当前状态的设计和操作,以达到改善钢坯加热的温度安排。同侧切换燃烧方式的蓄热式加热炉的速度和温度分布不能满足均匀快速的加热过程。钢坯的终端加热温度比前一种情况低30K。采用交叉切换燃烧模式可以改善流和温度的分布,交叉切换燃烧模式的钢坯的终端温度约为1 470 K,且内部的温差很小10K。

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